Updated: 2026-01-11
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0226U000407, (0125U000771) , R & D reports
Development of methanol production technology from various domestic raw materials to ensure energy independence of the state. Chapter 1. Development of catalysts and development of technological parameters of the process.
Розроблення каталізаторів для процесів отримання метанолу з синтез-газу та парової конверсії СО
Stryzhak Petro Ye., Доктор хімічних наук
08-01-2026
L. V. Pisarzhevskii Institute Of Physical Chemistry of The National Academy of Sciences of Ukraine
The purpose of this work is to develop heterogeneous catalytic processes for the conversion of various types of domestic raw materials into liquid synthetic motor fuel by methanol synthesis. For the process of obtaining methanol from synthesis gas obtained by gasification of various carbon-containing raw materials, it is planned to create metal oxide catalysts of a new generation. Determining the optimal conditions for such a process in combination with the optimization of the gasification process of solid carbon-containing raw materials will allow us to offer technological solutions for obtaining methanol from peat, solid bio-raw materials, solid household waste, etc. The proposed technological solutions will make it possible to create small modular converters of solid carbon-containing raw materials into methanol and synthetic motor fuel for operation in field conditions. The key task of creating small methanol plants is the development of design and engineering methods for the calculation of compact, technological and cheap catalytic reactors, simple and reliable in operation. It is planned to introduce the results of the project into production. The peculiarity of the composition of synthesis gas obtained by gasification of bio-raw materials is the increased content of carbon dioxide. Therefore, the steam reforming of CO, or the water shift reaction, is an important stage used to optimize the composition of the obtained synthesis gas.
Operational technological schemes of the methanol synthesis process have been developed, and the selection of main and auxiliary equipment has been carried out. Calculations for individual technological units have been performed. The structural design of the methanol synthesis process reactor has been developed, and its main and auxiliary characteristics have been calculated. The material and energy balance of the methanol synthesis process has been determined (depending on the composition of the synthesis gas). Сatalysts for the hydrogenation of carbon monoxide to methanol from synthesis gas have been selected, and their physicochemical characteristics have been determined using low-temperature nitrogen adsorption and Raman spectroscopy methods. To determine the optimal catalyst, test trials of catalyst samples in the methanol synthesis process under standard conditions were conducted on a laboratory setup.
Andrii I. Trypolskyi
Nina V. Vlasenko
Ihor B. Bychko
Oleksii O. Zhokh
Olha Z. Didenko
Lidiia Y. Dolhikh
Larysa O. Stara
Iryna L. Stoliarchuk
Valentyna I. Hrytsenko
Tamila H. Serebrii
Yurii M. Yefymenko
Viktoriia V. Nosach
Danylo S. Fatieiev
Vladyslav Y. Stets
Mykola O. Yukhno
2026-01-08
Updated: 2026-01-11
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